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United States Patent |
5,700,369
|
Zhou
,   et al.
|
December 23, 1997
|
Process for adsorboaggregational flotation of Carlin type natural gold
ore dressing
Abstract
A novel process for adsorptive aggregation and also floatation of Carling
type gold ores, which goes far beyond the conventional floatation method.
Said novel technological procedures comprise fine grinding as well as
sluicing of raw ores and adding special floatation agents such as
stripping agent, adsorptive aggregation agent as well as collecting agent
and flocculant in the course of coarse screening and sweep screenings. The
fine ore obtained using the present process is graded as 22 g/T with a
recovery yield langer than 83%. Said process has a screening index high
and stable, it is safe and reliable and can be effectively put into
industrial production.
Inventors:
|
Zhou; Zheng (Guangzhou, CN);
Zou; Zailan (Guangzhou, CN)
|
Assignee:
|
Guangzhou Institute of Geochemistry Chinese Academy of Sciences (Guangzhou, CN)
|
Appl. No.:
|
783012 |
Filed:
|
January 14, 1997 |
Current U.S. Class: |
209/166; 209/167 |
Intern'l Class: |
B03D 001/02; B03D 001/01 |
Field of Search: |
209/166,167
|
References Cited
U.S. Patent Documents
2512669 | Jun., 1950 | Morrow.
| |
4853114 | Aug., 1989 | Lewis.
| |
5030340 | Jul., 1991 | Panzer.
| |
Foreign Patent Documents |
85 1 09643 A | Apr., 1987 | CN.
| |
86 1 01495 A | Jun., 1987 | CN.
| |
86 1 01573 A | Jun., 1987 | CN.
| |
86 1 05982 A | Apr., 1988 | CN.
| |
1080567 A | Jan., 1994 | CN.
| |
Primary Examiner: Lithgow; Thomas M.
Attorney, Agent or Firm: Armstrong, Westerman, Hattori, McLeland & Naughton
Claims
We claim as our invention:
1. A novel process for adsorptive aggregation and floatation of Carling
type mine natural gold ores, comprising the following procedures:
(1) above 80% mineral ores are finely ground to smaller than 200 mesh;
(2) the mineral ores after being ground are first sluiced;
(3) then the sluiced ores are carried out a floatation which comprises
coarse screening and sweep screenings, wherein the following preparations
are sequentially added:
a. a stffficient amount of "the stripping agent" is added, the composition
(weight percentage) of which is: 0.025.about.1 fiuorosodium silicate,
0.03.about.1 lactic acid, 0.03.about.1.6 lead nitrate, 0.4.about.5 acid,
and the rest water;
b. a sufficient amount of "the adsorptive aggregation agent" wherein the
composition (weight percentage) is: 5.about.20 coal oil, 0. 1.about.3
machine oil, 0.1.about.2 turpentine oil, 0.1.about.1 ethyl xanthine,
0.05.about.0.5 dodecylamine and the rest water;
c. a sufficient amount of "xanthine collecting agent";
d. a sufficient amount of "flocculant".
2. The process of chaim 1 wherein the floatation comprises firstly one
coarse screening and subsequently two sweep screenings.
3. The process of claim 1 or claim 2 wherein the additions of the
preparations for each ton of mineral ores in the coarse screening of said
floatation are: stripping agent 0.3.about.0.7 kg, adsorptive aggregation
agent 0.6.about.1.0 kg, xanthine collecting agent 0.1.about.0.3 kg,
flocculant 0.02.about.0.07 kg; and the additions of the preparations for
each ton of mineral ores in the sweep screening are: stripping agent
0.15.about.0.35 kg, adsorptive aggregation agent 0.3.about.0.5 kg,
xanthine collecting agent 0.05.about.0.15 kg, flocculant 0.01.about.0.03
kg.
4. The process of claim 1 wherein the said "stripping agent" is
prescribeally prepared as follows:
a. fluorosodium silicate solution A of a prescribed concentration range of
0.1.about.4.0%;
b. lactic acid solution B of a prescribed concentration range of
0.12.about.4.0%;
c. lead nitrate solution C of a prescribed concentration range of
0.11.about.5.4%;
d. acid solution D of a prescribed concentration range of 1.5%.about.20%;
e. A is first mixed with B, then C is mixed with D, and finally A+B is
mixed with C+D.
5. The process of claim 1 or 4 wherein the acid in the ingredients of the
"stripping agent" is sulfuric acid or nitric acid.
6. The of claim 1 wherein the said "adsorptive aggregation agent" is
prescribedly prepared according to the following procedures:
a. ethyl xanthine and dodecylamine are dissolved in water to form the
aqueous solution E, the composition (weight percentage) of which is:
0.2.about.2 acetyl xanthine, 0.05.about.0.5 dodecylamine and the rest
water;
b. machine oil, turpentine oil, dodecylamine and water are added into coal
oil and mixed up homogeneously, the composition thereof: coal oil 10-40,
machine oil 0.2.about.6, turpentine oil 0.2.about.4, dodecylamine
0.05.about.0.5 and water the rest;
c. the mixture solution produced by step b is set static until it is
clearly delaminated, then the lower layer solution is removed and water of
same weight as that of lower layer solution is supplemented therein to
form a new mixture solution F;
d. E and F are simultaneously added into a container, basically according
to the ratio (weight) of 1:1 to be emulsified.
7. The process of claim 1 wherein the said "xanthine collecting agent" is a
xanthine mixture, consisting of ethyl xanthine, butyl xanthine, and
isopentyl xanthine, the composition thereof (weight percentage): ethyl
xanthine 20.about.40, butyl xanthine 20.about.40, and isopentyl xanthine
20.about.40.
8. The process of claim 1 wherein the flocculant is polyacrylamide, dextrin
or starch.
9. The process of claim 1 wherein the concentration of said flocculant is
0.01.about.0.1%.
Description
DESCRIPTION
The present invention relates to the improvement of gold ore screening
process.
The Carling type gold mine, i.e., the fine grain type gold mine, is a type
of natural gold, which distributes in a supermicroscopic state in the
sulfide mineral and the clay mineral, and contains a certain amount of
arsenic and carbon and other harmful impurities. It is a gold mine
typically not easy to be disposed both the screening enrichment and the
smelting recovery, of which are rather diffcult. If this sort of gold mine
employs conventional method to directly sinter-cyanide raw gold ores for
extractlong of gold, it tums out to be difficult to be applied in
production, because the raw gold ore is of no high grade, needing in
general to be sintered twice to achieve homogeneity, and the fine grain
gold is easy to be lost while being sintered etc. For the time being, the
process being under research is the floatation-sintering-cyaniding
process, the essentials of which are improving the grade of gold ore by
means of gold ore floatation, and merely sintering and cyanizing the fine
gold ore to obtain gold. This is a practical technological solution of
high efficiency and low cost, the key of its success lies in the gold ore
screening indices. Although a great many scientists and technicians have
conducted a great number of experimental studies on the floatation method
of Carling type mine natural gold ores, yet all of them fail to go beyond
the scope of "conventional floatation", that is, using the approach to
float the "visible natural gold" to solve the problem on floating the
"invisible natural gold". At present, the floatation indices that the
floatation experiments on Carling type mine natural gold ores can achieve
read:while the grade of raw gold ore is 3.91 g/T, the grade of fine gold
ore reaches about 9.18 g/T, the yield is about 37%, the fine gold ore
recovery is about 87% and the grade of the ore dregs is 0.81 g/T, these
are difficult to meet the requirement of industrial production.
The object of the present invention is to provide a novel floatation
process which can greatly raise the indices of the fine ore grade, has a
safe and reliable technology and a high and stable screening index, and is
suitable for the use of low grade gold ore, low grade gold-containing
dregs, especially Carling type mine natural gold ore to be practically and
effecively used in production.
The technical solution of the present invention is a novel
adsorption-aggregation-floatation process, the screening course of which
comprises the following steps.
1. About 80% of the mineral ore is first finely ground to below 200 mesh;
2. The mineral ore after being ground is sluiced;
3. Then the sluiced mineral ore is sent to the floatation machine system
for floataton comprising coarse screening and sweep screenings, in general
one coarse screening and two sweep screenings. During the screenings,the
following preparations shall be sequentially added there- into:
a. a sufficient amount of "stripping agent",a mixed aqueous solution of
fluorosodium silicate, lactic acid, lead nitrate and acid, the
compositions (weight percentage) of which is: 0.025.about.1 fluorosodium
silicate, 0.03.about.1 lactic acid, 0.03.about.1.6 lead mitrate,
0.4.about.5 nitric acid, and the rest water;
b. a sufficient amount of "adsorptive aggregation agent," a mixed
emulsified solution of ethtyl xanthine, coal oil, machine oil, turpentine
oil and dodecylamine, the composition (weight percentage) of which is: 520
coal oil, 0.1.about.3 machine oil, 1.about.2 turpentine oil, 0.1.about.1
ethyl xanthine, 0.05.about.0.5 dodecylamine and the rest water;
c. a sufficiant areout of "xanthine collecting agent;"
d. a sufficient amount of flocculant.
The acid in the ingredients of the "stripping agent" is preferably sulfuric
acid or nitric acid.
After one coares screening and two sweep screenings, the final fine ore and
ore dregs can be obtained,
The above-indicated technology is used, mainly based on the following
floating features of the Carling type mine natural gold ore :(1) the
sludge amount contained is large, mainly of clay mineral and carboneous
substance; (2) the floating properties of the gold-bearing minral,
i.e.pyrite, are very poor and difficult to be activated; (3) the
floatability of another gold-bearing mineral, the clay ore, is nice; (4)
the floating activity of the vein mineral ore is strong and difficult to
be inhibited etc. Among the procedures, that above 80% raw ore is finely
ground to smaller than 200 mesh is for the purpose of achieving a better
floatation effect; that the ore is first sluiced before floatathion is for
the purpose of sluicing those fine muddy dusts of average gold content
between 0.3 and 0.5 g/T so as to reduce the use amounts of the
preparations during the floatation, this is a critical step to raise the
floatation indices. The sluice operation generally uses dedust hopper
which is installed between the ore grinding machine and the floatation
stir basin, wherein the sluiced amount is controlled by the magnitude of
the up going water flow. The "stripping agent" and the "adsorptive
aggregation agent" uniquely and creatively added during the floatation,
are also important features of the present invention. The "stripping
agent" is used for cleansing the surface of pyrite so as to increase its
activity and so as to have the xanthine collecting agent later added
capable of being fixedly attached, it can further remove the surface
activity centers of the vein mineral ore so as to have the water film
fixedly covering thereon. The "adsorptive aggregation agent" acts to
absorptively accumulate the gold-containing minereal ore distributed in
the ore pulp.
The preparations to be added during above-mentioned floatation course are
determined by their corresponding use amounts, based on the different
sources of the ore samples, the usual preparation additions (for each ton
of mineral ore) during the coarse screening are: stripping agent
0.3.about.0.7 kg, adsorptive aggregation agent 0.6.about.1.0 kg, xanthine
collecting agent 0.1.about.0.3 kg, flocculant 0.02.about.0.07 kg, and
those during the sweep screening are: stripping agent 0.15.about.0.35 kg,
adsorptive aggregation agent 0.3.about.0.5Skg, xanthine collecting agent
0.05.about.0.015 kg, and flocculant 0.01-0.03 kg.
The said "stripping agent" and the said "adsorptive aggregation agent" are
special preparations to be added in the floatation system of the present
invention. Usually, the "stripping agent" is prescribedly prepared
according to the following method so as to achieve a better predetermined
effect:
a. fluorosodium silicate solution A of a prescribed concentration range
0.1%.about.4.0%.
b. lactic acid solution B of a prescribed concentration range
0.12%.about.4.0%;
c. lead nitrate solution C of a prescribed concentration range
0.11%.about.5.4%;
d. acid solution D of a prescribed concentration range 1.5%.about.20%;
e. A and B are first mixed up, then C and D are mixed, finally A+B and C+D
are mutually mixed up.
The adsorptive aggregation agent can be prescribed and prepared as follows:
a. ethyl xanthine and dodecylamine are dissolved in water to form aqueous
solution E the composition (weight percentage)of which reads: 0.2.about.2
ethyl xanthine, 0.05.about.0.5 dodecylamine and the rest water;
b. machine oil, turpentine oil, dodecylamine and water are added into coal
oil, and mixed up homogeneously, their composition (weight percentage)
reads: coal oil 10.about.40, machine oil 0.2.about.6, turpentine oil
0.2.about.4, dodecylamine 0.05.about.0.5 and water the rest;
c. the mixed solution produced by step b is set static until it is clearly
laminated, the main component of the lower layer solution is water which
contains the impurities released from various components of the mixture
solution. This portion of lower layer solution is removed, and water of a
same weight as that of the lower layer solution removed is supplemented to
form a new mixture solution F, and the action of this step is practically
to remove therefrom the impurities contained in the various components of
the mixture.
d. E and F are simultaneously added into the container to be emulsified,
basically according to the ratio (weight) 1:1.
The present invention uses the mixture xanthine consisting of ethyl
xanthine, butyl xanthine, and isopentyl xanthine as the "xanthine
collecting agent", the effect of which is much better than that of the
collecthing agent having but a single component, said mixture "xanthine
colleching agent" can be mixedly prepared according to the following
prescription (weight percentage): ethyl xanthine 20.about.40, butyl
xanthine 20.about.40 and isopentyl xanthine 20.about.40.
The flocculant to be added into the floatation system can be a substance
selected from the group consisting of polyacrylamide, dextrin and starch.
The concentration of the flocculant to be added into the floatation system
needs be adjusted to be 0.01.about.0.1%.
When the screening technology of the present invention is used for the
floatation of Carling type mine material gold ore, the grade of the fine
ore obtained is above 22 g/T, the recovery is larger than the grade index
of the fine ore resulted from conventional screening technologies,
further, the yield is nearly same, the screening indices of the entire
technology are high and stable, all the preparations used therein are not
toxic, giving rise to no environmental pollution, the procedures of said
process are clear cut, easy to be handled, and of lower investment, can be
effectively put into industrial production, and lead to significant
economic benefits.
EMBODIMENT EXAMPLE I
The adsorptive aggregation and floatation is conducted, based on the
following technological proceduses:
(1) the gold ores are roughly crushed and then machine ground to smaller
than 200 mesh up to 85%;
(2) the raw ores after being ground are sluiced to remove the fine maddy
dust of an average gold content smaller than 0.5 g/T;
(3) the gold ores after being sluiced are added into the floatation machine
for their floatations, first one coarse screening and then two sweep
screenings.
The following preparations are added thereinto during the coarse screening
and the sweep screenings:
a. preparations additions during coarse screening: stripping agent 0.5
kg/T, adsorptive aggregation agent (emulgive) 0.8 kg/T, xanthine
collecting agent 0.2 kg/T, polyacrylamide fiocculant 0.05 kg/T;
b. preparations additions during sweep screenings: stripping agent 0.25
kg/T, adsorptive aggregation agent (emulsive) 0.4 kg/T, xanthine
collecting agent 0.1 kg/T, polyacrylamide fiocculant 0.02 kg/T.
Among them, the stripping agent is prescribecdlly prepared according to the
following components (weight percentage): fiuorosodium silicate 0.5,
lactic acid 0.5, lead nitrate 0.8, sulfuric acid 2.about.7 and the rest
water. The prescription runs as follows: (1) fluorosodium silicate
solution A of a concentration 2% is prepared prescribedly; (2) lactic acid
solution B of a concentration 2% is prepared prescribedly; (3) lead
nitrate solution C of a concentration concentration 3.2% is prepared
prescribedly; (4) sulfuric acid solution D of a concentration 10.8% is
prepared prescribedly; (5) A is mixed with B, then C is mixed with D, and
finally A+B is mixed with C+D.
The composition of the adsorptive aggregation agent (weight percentage)
reads: 11.7 coal oil, 1.0 machine oil, 0.6 turpentine oil, 0.5 ethyl
xanthine, 0.1 dodecylamide and the rest water.
The prescription of the adsorptive aggregation agent runs as follows:
a. ethyl xanthine and dodecylamide are dissolved into water to form aqueous
solution E, the composition (weight percentage) of said aqueous solution
reads: 10 ethyl xanthine, 0.1 dodecylamine and the rest water;
b. machine oil, turpentine oil, dodecylamine and water are added into coal
oil, and homogeneously mixed up, the composition (weight percentage)
thereof is: 23.40 coal oil, 2 machine oil, 1.2 turpentine oil, 0.1
dodecylamine and the rest water;
c. the mixture solution produced by step b is set static until said
solution is clearly laminated, the lower layer water containing impurities
is removed and then water of same amount as that of removed lower layer
solution is supplemented thereinto to obtain new mixture solution F;
d. E and F are simultaneously added into the container to be emulsified,
basically according to the ratio 1:1 (weight percentage).
The xanthine collecting agent is formed by mixing ethyl xanthine, butyl
xanthine and isopentyl xanthine according to the prescribed ratio 1:1:1.
The concentration of the polyacrylamide flocculant is adjusted to be 0.05%.
EMBODIMENT EXAMPLE II
The adsorptive aggregation and floatation technological procedures are same
as those of Embodiment Example I, the preparations additions during the
coarse screening and the sweep screenings are:
a. preparations addtions during coarse screening: stripping agent 0.3 kg/T,
adsorptive aggregation agent (emulsive) 0.6 kg/T, xanthine collecting
agent 0.1 kg/T, and dextrin flocculant 0.02 kg/T;
b. preparations additions during sweep screenings: stripping agent 0.15
kg/T, adsorptive aggregation agent(emulsive) 0.3 kg/T, collecting agent
0.05 kg/T and dextrin flocculant 0.01 kg/T.
Among them, the stripping agent is prescribedly prepared according to the
following composition (weight percentage): 1.0 fluorosodium silicate, 1.0
lactic aid, 1.6 lead nitrate, 5.0 sulfuric acid and the rest water. The
prescription thereof runs as follows: (1) 4.0% fluorosodium silicate
solution A is prescribedly prepared; (2) 4.0% lactic acid solution B is
prescribedly prepared; (3) 5.4% lead nitrate C is prescribdedly prepared;
(4) 20% sulfuric acid solution D is prescribedly prepared; (5) A is mixed
with B, then C is mixed with D and finally A+B is mixed with C+D.
The composition (weight percentage) of the adsorptive aggregation agent
reads: coal oil 20, machine oil 3, turpentine oil 2, ethyl xanthine 1,
dodecylamine 0.5 and water the rest.
The prescription of the adsorptive aggregation agent runs as follows:
a. ethyl xanthine and dodecylamine are dissolved in water to form aqueous
solution E, the composition (weight percentage) of said aqueous solution
reads: 2 ethyl xanthine, 0.5 dodecylamine and the rest water;
b. machine oil, turpentine oil, dodecylamine and water are sequentially
added into coal oil and mixed up homogeneously, the composition thereof
(weight percentage) reads: 40 coal oil, 6 machine oil, 4 turpentine oil,
0.5 dodecylamine and the rest water;
c. the mixture solution produced by step b is set static until said
solution is clearly laminated, water of the lower layer containing
impurities is removed to form new mixture solution F;
d. E and F are simultaneously added into a container to be emulsified
according to the weight ratio 1:1.
The xanthine collecting agent is formed by mixing the followings (weight
percentage): ethyl xanthine 20, butyl xanthine 40, isopentyl xanthine 40.
The concentration of the dextrin flocculant is adjusted to be 0.1%.
EMBODIMENT EXAMPLE III
The adsorptive aggregation and floatation technological procedures are same
as those of Embodiment Example I, the preparations additions during the
coarse screening and the sweep screenings read as follows:
a. preparations additions during coarse screening: stripping agent 0.7
kg/T, adsorptive aggregation agent (emulsive) 1.0 kg/T,xanthine collecting
agent 0.3 kg/T,and starch flocculant 0.07 kg/T;
b.preparations additions during sweep screenings: stripping agent 0.35
kg/T,adsorptive aggregation agent (emulgive) 0.5 kg/T, xanthine collecting
agent 0.15 kg/T, starch flocculant 0.03 kg/T.
Among them, the stripping agent is prescribedly prepared according to the
following composition (weight percentage): 0.025 fluorosodium silicate,
0.03 lactic acid, 0.03 lead nitrate, 0.4 acid and the rest water. The
prescription of the stripping agent runs as follows: (1) fluorosodium
silicate A of a concentration 0.1% is prepared prescribedly; (2) lactic
acid solution B of a concentration 0.12% is prepared prescribedly; (3)
lead nitrate solution C of a concentration 0.1% is prepared prescribedly;
(4) diluted acid solution D of a concentration 1.5% is prepared
prescribedly; (5) A is first mixed with B, then C is mixed with D and
finally A+B and C+D are mutually mixed up.
The compostion (weight percentage) of the adsorptive aggregation agent
reads: 5 coal oil, 0.1 machine oil, 0.1 turpentine oil, 0.1 ethyl
xanthine, 0.05 dodecylamine and the rest water. The prescription thereof
runs as follows: a). ethyl xanthine and dodecylamine are dissolved in
water to form aqueous solution E, the composition (weight percentage)of
which reads: 0.2 ethyl xanthine, 0.05 dodecylamine and the rest
water;b).first machine oil, turpentine oil, dodecylamine and water are
added into coal oil, and homogeneously mixed up, with the composition
thereof (weight percentage) being: 10 coal oil, 0.2 machine oil, 0.2
turpentine oil, 0.05 dodecylamine and the rest water; c).the mixted
solution produced by step b is set static until it is clearly laminated,
the lower layer solution thereof is removed and then water of same weight
as that of the lower layer solution is supplemented thereinto to form new
mixture solution F; d).E and F are simultaneously added into a container
to be emulsified, basically according to the ratio(weight ratio) 1:1.
The xanthine collecting agent is prescribed by mixing the following
components: ethyl xanthine 40, butyl xanthine 38, and isopentyl xanthine
22.
The concentration of the starch flocculant is adjusted to be 0.01%.
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